Annex I - VERTIC
Annex I - VERTIC
Annex I - VERTIC
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▼M2<br />
0B003 Plant for the conversion of uranium and equipment specially<br />
designed or prepared therefor, as follows:<br />
a. Systems for the conversion of uranium ore concentrates to<br />
UO 3 ;<br />
b. Systems for the conversion of UO 3 to UF 6 ;<br />
c. Systems for the conversion of UO 3 to UO 2 ;<br />
d. Systems for the conversion of UO 2 to UF 4 ;<br />
e. Systems for the conversion of UF 4 to UF 6 ;<br />
f. Systems for the conversion of UF 4 to uranium metal;<br />
g. Systems for the conversion of UF 6 to UO 2 ;<br />
h. Systems for the conversion of UF 6 to UF 4 ;<br />
i. Systems for the conversion of UO 2 to UCl 4 .<br />
0B004 Plant for the production or concentration of heavy water,<br />
deuterium and deuterium compounds and specially designed or<br />
prepared equipment and components therefor, as follows:<br />
a. Plant for the production of heavy water, deuterium or<br />
deuterium compounds, as follows:<br />
1. Water-hydrogen sulphide exchange plants;<br />
2. Ammonia-hydrogen exchange plants;<br />
b. Equipment and components, as follows:<br />
1. Water-hydrogen sulphide exchange towers fabricated from<br />
fine carbon steel (e.g. ASTM A516) with diameters of 6 m<br />
to 9 m, capable of operating at pressures greater than or<br />
equal to 2 MPa and with a corrosion allowance of 6 mm<br />
or greater;<br />
2. Single stage, low head (i.e. 0,2 MPa) centrifugal blowers or<br />
compressors for hydrogen sulphide gas circulation (i.e. gas<br />
containing more than 70 % H 2 S) with a throughput capacity<br />
greater than or equal to 56 m 3 /second when operating at<br />
pressures greater than or equal to 1,8 MPa suction and<br />
having seals designed for wet H 2 S service;<br />
3. Ammonia-hydrogen exchange towers greater than or equal<br />
to 35 m in height with diameters of 1,5 m to 2,5 m capable<br />
of operating at pressures greater than 15 MPa;<br />
4. Tower internals, including stage contactors, and stage<br />
pumps, including those which are submersible, for heavy<br />
water production utilising the ammonia-hydrogen exchange<br />
process;<br />
5. Ammonia crackers with operating pressures greater than or<br />
equal to 3 MPa for heavy water production utilising the<br />
ammonia-hydrogen exchange process;<br />
6. Infrared absorption analysers capable of on-line hydrogen/<br />
deuterium ratio analysis where deuterium concentrations are<br />
equal to or greater than 90 %;<br />
7. Catalytic burners for the conversion of enriched deuterium<br />
gas into heavy water utilising the ammonia-hydrogen<br />
exchange process;<br />
8. Complete heavy water upgrade systems, or columns<br />
therefor, for the upgrade of heavy water to reactor-grade<br />
deuterium concentration.<br />
2009R0428 — EN — 15.06.2012 — 002.001 — 54